Polyesters containing chlorinated gem-dimethyl groups



United States Patent Off ICC 3,514,422 Patented May 26, 1970 3,514,422 POLYESTERS CONTAINING CHLORINATED GEM-DIMETHYL GROUPS John R. Caldwell and Winston J. Jackson, Jr., Kingsport,

Tenn., assignors to Eastman Kodak Company, Rochester, N.Y., a corporation of New Jersey No Drawing. Continuation-impart of application Ser. No. 347,053, Feb. 24, 1964. This application Mar. 25, 1968, Ser. No. 715,504

Int. Cl. C08f 27/02 U.S. Cl. 260-304 19 Claims ABSTRACT OF THE DISCLOSURE Polyesters useful as fibers and films and containing gemdimethyl groups are made self-extinguishing and soluble in low-boiling solvents (methylene chloride, chloroform, dioxane) by incorporating therein from about to about 50 percent by weight of chlorine, said chlorine replacing the hydrogen atoms of said gem-dimethyl groups.

This application is a continuation-in-part of Caldwell and Jackson U.S. Ser. No. 347,053; filed Feb. 24, 1964 now abandoned.

This invention relates to novel, polymeric compositions and their preparations, and particularly concerns novel polyesters exhibiting a multiplicity of improved properties.

A great many polyesters, unfortunately, have one or more drawbacks, such as being highly flammable or insoluble in low-boiling solvents such as methylene chloride, chloroform, and dioxane. The limitations imposed by their flammability are, of course, obvious. These flammable polyesters find little use in fibers and films to be employed near open flames. Regarding their insolubility, they can only practicably be spun into fibers from their melts, which is costly and can lead to a certain amount of thermally induced degradation. Moreover, they cannot conveniently be cast or spun from the non-volatile solvents, such as tetrachloroethane and the like, in which they may be soluble because of the time and heat required to evaporate these solvents. In this regard, it is noted that the sustained heat required for drying solvents such as cresol, 'y-butyrolactone, and ethylene carbonate, which boil above 200 C. and are employed to solubilize polyethylene terephthalate, can lead to considerable polymer degradation.

Objects of the present invention, therefore, are: to provide polyesters having good heat and hydrolytic stability and which exhibit significantly improved non-flammability and solubility characteristics; to provide polyesters which can be readily solubilized at relatively low temperatures and solution spun or otherwise formed; and to provide a commercially practicable process for preparing these polymers.

These and other objects in a general sense have been achieved in accordance with the present invention through the discovery that when polyesters containing relatively large amounts of gem-dimethyl groups are chlorinated by the process hereinafter disclosed, they become non-flammable and soluble in low-boiling solvents. In a more specific sense, the objects are achieved through the discoveries; j

(1) that chlorine can be introduced into the preferred polyesters by chlorination of some of the methyl groups of the recurring gem-dimethyl groups in the structures:

to form --CH Cl and --CHC1 groups and leave some -:-CH groups without causing excessive polymer degradatlon;

(2) that such chlorination, to the proper degree, imparts the aforesaid desirable properties to the polymers as well as rendering them more thermally stable; and

(3) that the more difiicultly soluble polymers may be readily solubilized by a novel solvent system hereinafter disclosed, and thereby rendered readily chlorinatable.

By the term gem-dimethyl group, we refer to the situation wherein two methyl groups are attached to the same carbon atom. These two methyl groups may then be referred to as gem-dimethyl groups.

The present polymers may be defined, therefore, as a polymeric composition having an inherent viscosity of at least about 0.3, as measured at 25 C. using 0.25 gram of polymer in 100 ml. of chloroform, said polymeric composition containing at least about percent by weight of a recurring structural unit selected from the group consisting of:

wherein R is a member selected from the group consisting of radicals of the formulas:

CH CH and CH; CH;

and wherein R is a member selected from the group con sisting of a direct carbon-to-carbon bond and divalent radicals of the formulas:

wherein the hydrogen atoms of the gem-dimethyl groups have been replaced by chlorine in an amount such that said polymeric composition contains from about to about 50 percent by weight of chlorine.

The

form of polymer is derived from the interaction of pivalolactone in the presence of catalytic amounts of a tertiary amine or acidic catalysts. The polymer may also be obtained by the self-condensation of hydroxypivalic acid. Because this polymer is very highly crystalline, it has little utility for fibers and molded, extruded, or pressed objects, and cast films thereof are brittle. Moreover, this polymer is insoluble in such relatively low-boiling solvents as methylene chloride, chloroform, and dioxane and, therefore, is difiicult to cast into films and surface coatings which require, from a practical standpoint, rapid solvent evaporation.

Desirably, the degree of chlorine substitution is sufii cient to give a chlorine content of between about 5 to 50 percent by weight of the polymer with between about 15 and about 40 percent by weight being preferred for most polymers. It is noted that precise quantitative analysis of CH Cl and -CHC1 group content is very difiicult. However, it has been ascertained by nuclear magnetic resonance (NMR) that as between the two, the CH Cl groups predominate in the polymer. It is noted that where relatively low-average chlorine substitution is achieved, substantial amounts of -CH groups are present, and where relatively high-average chlorine substitution is achieved, substantial amounts of -CHC1 groups are present. Of particular interest is the fact that the NMR analysis indicated practically no chlorine substitution on the aromatic rings. Therefore, NM R shows that it is the hydrogen atoms of the gem-dimethyl groups which have been replaced by chlorine.

The more conventional types of polyester reactants such as aliphatic dibasic acids and glycols may be co-reacted with diols and dibasic acids; however, the most thermally and hydrolytically stable polyesters are those containing at least about 80 percent by weight of the aforesaid preferred reactants. It is noted that the aromatic dibasic acid component may consist of up to 30 mole percent of oxalic or dimethylmalonic acid since neither of them present CH groups in the polymer chain.

The chlorination procedure comprises passing chlorine into solutions of the polymers in chlorinated hydrocarbons while illuminating with visible or ultraviolet light or while periodically adding a free-radical catalyst selected from the group, for example, of inorganic peroxygen, organic peroxygen, azo, and redox compounds. Examples of such catalysts are potassium persulfate; benzoyl peroxide; a,u'-azobisisobutyronitrile; and ammonium persulfate-sodium 'bisulfite. It is sometimes advantageous to use both a catalyst and illumination. The reaction may be carried out at 0 to 100 C., but temperatures of to 40 C. are normally used. Appreciable degration of the polymers takes place at the higher temperatures, and chlorination proceeds very slowly at lower temperatures. Other chlorinating agents such as sulfuryl chloride, phosphorus pentachloride, and t-butyl hypochlorite may be used, but chlorine is most effective.

In the case of polyesters of tetramethylcyclobutanediol which are insoluble in the low-boiling chlorinated hydrocarbons such as methylene chloride and chloroform, it is necessary to use tetrachloroethane or pentachloroethane as the solvent for these polymers. It is usually possible to dissolve the polyesters of dimethylpropanediol in lowboiling solvents, but the chlorination is often more efficient when tetrachloroethane or pentachloroethane is employed since less chlorination of these solvents occurs.

It is not necessary for an HCl acceptor to be present in the system, but it is often advantageous to use water to remove the HCl from the organic phase and/or powdered calcium carbonate to neutralize the HCl. Less breakdown of the polymer during chlorination then occurs. After completion of the chlorination, the organic layer is washed with sodium bicarbonate solution to ensure neutralization of all of the HCl which has formed. If calcium carbonate is used in the reaction mixture and some carbonateremains, it is first removed by filtration or by adding a little acetic acid. After the polymer solution is thoroughly washed with Water to remove all salts, it is slowly added to methyl alcohol or some other non-solvent to precipitate the polymer as a white fibrous product.

The preferred chlorination solvent is tetrachloroethane, but some of the polyesters are insoluble in this solvent; e.g., polypivalolactone and the polyester from terephthalic acid and trans 2,2,4,4-tetramethyl 1,3-cyclobutanediol. These polymers can be dissolved, however, if trichloroacetic or trifluoroacetic acid is added (5 to 50 percent by Weight of the solvent mixture, depending upon the polymer). For example, polypivalolactone is not soluble in any of the common solvents, but is soluble in about 8/1 (by volume), methylene chloride/trifluoroacetic acid. When the polymer in this mixture is chlorinated, appreciable chlorination of the methylene chloride also occurs. The solvent system 83/17 (by weight), tetrachloroethane/trichloroacetic acid is chlorinated to a substantially less degree. Trichloroacetic acid and trifiuoroacetic acid also increase the solubility of polyesters in saturated chlorinated hydrocarbons containing one to three carbon atoms and at least two chlorine atoms; e.g., methylene chloride, ethylene dichloride, chloroform, methylchloroform, tetrachloroethane, pentachloroethane, and pentachloropropane. When these trihalo acids are employed, water is not added because the trihalo acids are soluble in water, and calcium carbonate is not added because it reacts with the acid.

Under the conditions employed in chlorinating these polyesters substantially no chlorination of the aromatic rings occurs. The chlorinated polymers consist of mixtures containing --CH Cl groups, unchlorinated --CH groups, and -CHC1 groups. Normally, the polymers become self-extinguishing when at least about 28 percent by weight of chlorine is present therein. By selfextinguishing it is meant that a film of the polymer stops burning practically immediately when it is removed from a flame. Polymers containing more chlorine are even more resistant to burning. The polyesters of 2,2-dimethyl-1,3-propanediol are normally soluble in low-boiling solvents such as methylene chloride. The polyesters of 2,2,4,4 tetramethyl 1,3 cyclobutanediol, on the other hand, are usually insoluble in such solvents, but the polymers containing 10 to 20 percent chlorine are soluble. These chlorinated polymers can be readily cast into films or spun into fibers from such solvents. Chlorinated polypivalolactone containing an average of about one chlorine atom per recurring unit is soluble in methylene chlorine, and clear, tough films can be cast from the dope. When this polymer is chlorinated to an average of about two chlorine atoms per recurring unit, it is non-burning.

Chlorination of the polyesters increases the dielectric constants thereof and makes them more valuable for use as dielectrics. For example, the unchlorinatetd polyester of terephthalic acid and 2,2,4,4-tetramethyl-1,3-cyclobutanediol has a dielectric constant of 2.9 at 1 kc., whereas the polymer containing 30 percent chlorine has a dielectric constant of 3.6 at 1 kc. The heat stability of the chlorinated polyesters can be improved by adding 0.1 to 4 percent of a compound of one or more of the following types: organo tin sulfur, organo tin, epoxy, azirdinyl, urea phosphite, unsaturated aliphatic, fatty acid salt (cadmium, zinc, or tin), or powdered calcium carbonate. They can be added to films by dissolving or suspending in the dope from which the film is cast. They may be added to the polymer by dissolving or suspending in the dope from which the film is cast. They may be added to the, polymer by dissolving or suspending in a solvent such as methanol in which the polymer is soluble, adding the polymer, and then evaporating to dryness,

In this invention, the inherent viscosity (I.V.) of the unchlorinated polymer is generally at least about 0.4, as measured at 25 C. using 0.25 gram of polymer per 100 ml. of a solvent composed of 60 percent phenol and 40 percent tetrachloroethane. The inherent viscosity of the chlorinated polymer is generally at least about 0.3, as measured at 25 C. using 0.25 gram of polymer per 100 ml. of chloroform. The polyesters of tetramethylcyclobutanediol were prepared with the commercially available diol containing about a 40/60 cis/trans ratio.

The following examples are included for a better understanding of the invention. In these examples, percentages of chlorine are by weight, based on the weight of the chlorinated polymer.

EXAMPLE 1 A polyester prepared from dimethyl terephthalate and 2,2,4,4-tetramethyl-1,3-cyclobutanediol is chlorinated by the following procedure. The polymer (25 grams, inherent viscosity of 0.85) is dissolved in 200 ml. of tetrachloroethane by stirring at 100 C. After solution is attained and the mixture is cooled to room temperature, 200 ml. of water and 9.0 grams of calcium carbonate powder are added. While the mixture is stirred and irradiated with a 275 watt ultraviolet lamp, 13 grams of chlorine measured as the weight loss of the chlorine lecture bottle, is added during 40 minutes. The temperature is maintained at 25 to 35 C. by cooling with a water bath. The organic layer is then separated and stirred with some acetic acid to remove a small amount of calcium carbonate which has not reacted. It is then stirred with aqueous sodium bicarbonate solutionto remove all acid.-.After the polymer solution is stirred with several portions of water, it is slowly added-to methyl alcohol to precipitate the polymer as awhite fibrous material. 'It'has an inherent viscosity of 0.58 and-a softening range of 205 to-2-16" C. The chlorine analysis'indicates that 20.3 percent chlorine is present The polymer, y vhich is not self extingpishi'ng, is soluble in methylene chloride. A film, cast from this solvent, has the following properties: tensile strength=9,9 p.s.i., elongation=l6 percent, modu1us==3.3 10 p.s.i., two percent heat distortion temperature (at 50 p.s.i.)= 196 C., dielectric constant (at one kc. and 25 to 150 C.)=3.-6-3.7, dissipation factor (at one kc. and 25 to 150 C.) :09 to 0.5 percent.

EXAMPLE 2- Example 1 is repeated but 50 percent more calcium carbonate and chlorine and added. The polymer has an inherent viscosity of 0.52 and a softening range of 218 to 220 C. The chlorinecontent of the polymer is 30.8 percent, indicating that somewhat over three chlorine atoms are present per diol unit. A film of the polymer, which is self-extinguishing, is cast from methylene chloride. It has the following properties: tensile strength: 9,800 p.s.i., elongation=17 percent, modulus=3.4 l0 p.s.i., two percent heat-distortion temperature (at 50 p.s.i.)=184 C., dielectric constant (at one kc. and 25 to 150 C.)=3.6-3.8, dissipation factor. (at,one kc. and 25 to 150 C.)=-1.2--0.6 percent.

EXAMPLE' 3 Example 1 is repeated with omission of the calcium carbonate and addition of 261 grams of chlorine. The polymer has an inherent viscosity of 0.37 and a softening range of 207 to 216 C. The chlorine content of-the polymer is 35 percent, indicating that about four chlorine atoms are present per diol unit. 'A-- fi1m .of the polymer, which is self-extinguishing, is cast from methylene chloride. It has the following properties tensile strength= 9,l00 p.s.i., elongation=11 percent, modulus=3.2 l0 p.s.i., two percent heat-distortion temperature (at 50 p.s.i.)=-170 C., dielectric constant (at one kc. and 25 to 150 C):

3.5-3.6, dissipation factor (at one kc. and 25 to 150 C.) =0.9-0.7 percent.

EXAMPLE 4 A procedure similar to that of Example 1 is used but with certain modifications. The polyester (27.4 grams) is dissolved in 300 ml. of tetrachloroethane, and 200 ml. of water and 0.5 gram of benzoyl peroxide are added. The mixture is held at 28 to 30 C. and illuminated with a 300 watt flood lamp (visible light). Chlorine is passed into the stirred mixture until the loss in weight of the cylinder is six grams. A small sample of polymer solution is removed, and one gram more of chlorine is added to the original mixture. The sample and reaction mixture are then worked up as in Example 1. The first sample, which is not completely soluble in methylene chloride, contains 7.1 percent chlorine. The second portion is completely soluble in methylene chloride. It contains 9.1 percent chlorine and has an inherent viscosity of 0.65. A film, cast from methylene chloride, has the following properties: tensile strength=8,700 p.s.i., elongation=30 percent, modulus=2.8 10 p.s.i., two percent heat-distortion temperature (at 50 p.s.i.) =186 C.

EXAMPLE 5 A polyester prepared from 2,2,4,4-tetramethyl-1,3-cy clobutanediol and the dimethyl ester of 2,6-naphthalenedicarboxylic acid is chlorinated according to the method of Example 1; however, visible illumination is used, and the calcium carbonate is omitted. To 25 grams of the polymer is added 25 grams of chlorine. A chlorine analysis of the produce indicates that 29.4 percent chlorine is present. The polymer has an inherent viscosity of 0.62 and a softening range of 240 to 250 C. It is self-extinguishing and soluble in methylene chloride. At one kc. and 25 to 150 C., a film has a dielectric constant of 3.5-3.7 and a dissipation factor of 1.0-0.7 percent.

EXAMPLE 6 A polyester prepared from 2,2,4,4-tetramethyl-1,3-cyclobutanediol and diphenyl carbonate is chlorinated according to the method of Example 1 but with the addition of benzoyl peroxide. Ten grams of the polymer .(inherent viscosity 0.52) and 0.5 gram of benzoyl peroxide are dissolved in tetrachloroethane, water and calcium carbonate are added, and 17 grams of chlorine are passed in. A chlorine analysis of the product indicates that 39.6 percent chlorine is present. The polymer has an inherent viscosity of 0.40 and a softening range of 180 to 200 C. A film of the polymer, which is self-extinguishing, is cast from methylene chloride. It has the following properties: tensile strength=9,600 p.s.i., elongation=4.9 percent, modulus=4.2 10 p.s.i., two percent heat-distortion temperature (at 50 p.s.i.) C. At one kc. and 25 to C. the film has a dielectric constant of 3.6-4.2 and a dissipation factor of 1.2-1.8 percent.

EXAMPLE 7 A polyester prepared from 2,2-dimethyl-1,3-propanediol and dimethyl terephthalate is chlorinated according to the method of Example 1 but with a reaction temperature of 10 C. To 16 grams of the polymer in tetrachloroethane are added 18 grams of chlorine. A chlorine analysis of the product indicates that 27.2 percent chlorine is present. The polymer has an inherent viscosity of 0.60 and a softening point of 120 C. It is selfextinguishing and soluble in methylene chloride. At one kc. and 25 C., a film has a dielectric constant of 3.5 and a dissipation factor of 0.8 percent.

and the dimethyl ester of 2,6-naphthalenedicarboxylic acid 7 is chlorinated according to the method of Example 1. To 28 grams of the polymer in tetrachloroethane are added 43 grams of chlorine. A chlorine analysis of the product indicates that 34.1 percent chlorine is present. The polymer has an inherent viscosity of 0.47 and a softening range of 150l60 C. It is self-extinguishing and soluble in methylene chloride. At one kc. and 25 C., a film has a dielectric constant of 3.6 and a dissipation factor of 1.2

percent.

EXAMPLE 9 Example 1 is repeated without illumination but with the addition of 0.5 gram of acetyl peroxide. Whenever the chlorination slows down, 0.2 gram more of acetyl peroxide is added. The final polymer has an inherent viscosity of 0.55 and a chlorine content of 19.2 percent.

EXAMPLE 10 Example 9 is repeated with azoisobutyronitrile instead of acetyl peroxide. Similar results are obtained.

EXAMPLE 1 1 Ten grams of polypivalolactone (inherent viscosity of 2.8) are dissolved in a mixture containing 200 ml. of methylene chloride and 25 ml. of trifluoroacetic acid. While this solution is irradiated with a 275 watt ultraviolet lamp and a water bath holds the temperature at 25 to 30 C., 35 grams of chlorine is passed in. The mixture is then neutralized by stirring with sodium bicarbonate powder. The polymer solution is thoroughly washed with water and slowly added to methanol. The polymer precipitates as a white fibrous material. It has an inherent viscosity of 1.35, contains 23 percent chlorine, and is soluble in methylene chloride. A film cast from this solvent has the following tensile properties: break strength=4,600 p.s.i., yield strength=4,400 p.s.i., elongation=217 percent.

EXAMPLE 12 Example 11 is repeated with a polymer solvent comprising a mixture containing 150 ml. of tetrachloroethane and 50 grams of trichloroacetic acid. The mixture is heated to 80 to 90 C. to dissolve the polymer, cooled to 30 C., and 35 grams of chlorine are added while the temperature is held at 30 to 35 C. The polymer is then washed and isolated as before. It has an inherent viscosity of 0.74, contains 40.8 percent chlorine, and is soluble in methylene chloride. A film, cast from this solvent, is tough, flexible, and non-burning according to ASTM test D 68-61.

EXAMPLE 13 Example 11 is repeated with a solvent comprising a mixture of 100 m1. of ethylene dichloride and 100 ml. of trifluoroacetic acid. The chlorinated polymer has an inherent viscosity of 1.18 and contains 24.2 percent chlorine. It is soluble in methylene chloride.

EXAMPLE 14 A polyester prepared from dimethyl terephthalate and the 3-hydroxy-2,2-dimethylpropyl ester of 3-hydroxy-2,2- dimethylpropionic acid is chlorinated by the procedure of Example 7. The product contains 22.6 percent chlorine and is soluble in methylene chloride. It is valuable as a fire-retardant protective coating.

The invention has been described in detail with particular reference to preferred embodiments thereof, but it will be understood that variations and modifications can be effected within the spirit and scope of the invention as described hereinabove and as defined in the appended claims.

We claim:

1. A polymeric composition having an inherent viscosity of at least about 0.3, as measured at 25 C. using 0.25 gram of polymer in 100 ml. of chloroform, said polymeric composition containing at least about '80 perwherein R is a member selected from the group consisting of radicals of the formulas:

and wherein R is a member selected from the group consisting of a direct carbon-to-carbon bond and divalent radicals of the formulas:

Q Q m @0130 wherein the hydrogen atoms of the gem-dimethyl groups have been replaced by chlorine in an amount such that said polymeric composition contains from about 5 to about 50 percent by weight of chlorine.

2. A composition as defined by claim 1 wherein R is the CH3 OH: H

CH3 CH3 radical and R is the radical.

3. A composition as defined by claim 1 wherein'R is the CH3 on, H

c 11 CQCH,

radical and R is the radical.

9 4. A composition as defined byi claim wherein is the A CH: CH:

radical and R' is the 7. A composition as defined by claim 1 wherein the gem-dimethyl groups are sufliciently chlorinated to render the composition self-extinguishing.

8. A fiber formed from a composition as defined by claim 1.

9. A film formed from a composition as defined by claim 1.

10. A molded article formed from a composition as defined by claim 1.

11. A composition as defined by claim 1 wherein the gem-dimethyl groups are sufficiently chlorinated to render the composition soluble in at least one solvent selected from the group consisting of methylene chloride and chloroform.

12. A viscous dope of a composition as defined by claim 1 in at least one solvent selected from the group consisting of methylene chloride, chloroform, and dioxane.

13. A process for forming shaped articles from a composition as defined by claim 1, said process comprising forming a dope of said composition in at least one solvent selected from the group consisting of methylene chloride, chloroform, and dioxane, forming said dope into a shaped article, and evaporating the solvent.

14. A process for chlorinating a difiicultly' soluble polymeric composition as defined by claim 1, said process comprising dissolving the polymeric composition in a solvent mixture comprising a chlorinated hydrocarbon of from one to three carbon atoms and at least about five percent by weight of a trihalo acid, and contacting the dissolved polymeric composition at a temperature of from about 10 to about 40 C. with chlorine in the presence of a chlorination promoter.

15. A polyester of dimethyl terephthalate and the 3- hydroxy-2',2-dimethylpropyl ester of 3-hydroxy-2,2-dimethylpropionic acid wherein the hydrogen atoms of the gem-dimethyl groups have been replaced by chlorine in an amount such that said polyester contains from about 5 to about 50 percent by weight of chlorine.

16. A process for chlorinating a polymeric composition, said process comprising contacting a polymeric composition containing at least about percent by weight of a recurring structural unit selected from the group consisting of:

-o-oH- ---o-- wherein R is a member selected from the group consisting of radicals of the formulas:

wherein R is a member selected from the group consisting of a direct carbon-to-carbon bond and divalent radicals of the formulas:

a... Q" Q LU @Q to with chlorine at from about 0 to about 50 C. in the presence of a chlorination promoter, said chlorinated polymeric composition having an inherent viscosity ofat least about 0.3, as measured at 25 C. using 0.25 gram,

of polymer" in ml. of chloroform, wherein the hydrogen atoms of the gem-dimethyl groups have been replaced in"-.an amount such that said polymeric composition contains from about 5 to about 50 percent by weight of chlorine.

17. A process as defined by claim 16 wherein the chlorination promoter is selected from the group consisting of ultraviolet radiation, visible light, and a free radical initiator.

18. A process as defined by claim 16 wherein suflicient water is present to reduce the concentration of HCl in the organic phase and hence the tendency of the polymer to hydrolyze.

19. A process as defined by claim 16 wherein CaCO 11 12 is dispersed in the reaction medium to neutralize the HCl 3,265,762 8/1966 Quisenberry 26075 formed. 3,320,336 5/1967 Duke et a1. 260-75 References MORRIS LIEBMAN, Primary Examiner UNITED STATES PATENTS 5 s. M. PERSON, Assistant Examiner 2,021,763 11/1935 Bauer 260-17 2,980,656 4/1961 Jones et a1 26085.1

3,249,652 5/1966 Quisenberry 260-75 260-333, 65, 75, 78.3, 79, 96

UNITED STATES PATENT OFFICE Patent N0. 14 422 Invenror(s) John R.

Dated Jul 1 l O Caldwell and Winston J. Jackson. Jr.

It is certified that error appears in the above-identified parent and that said Letters Parent are hereby corrected as shown below:

Column line 58, Column line 56, Column 6, line 33, Column 7, line 44,

Column Attest:

M. Fletcher, It.

Amazin Offioor EC V0261 10, lines 25-29,

"degration" should read ---degradation---. "chlorine" should read -chloride--- "produce" should read ---product---.

"35 C." should read --35C.---.

CH CH I -CH2-C-COOCH2-(|J-CH2- M88101! of Patents the formula should appear as shown below: 

